Abstract:
Die vorliegende Erfindung betrifft ein optomechanisches System (200) auf Basis von einer oder mehreren optomechanischen Elementarzellen (400), die Verwendung des optomechanischen Systems zur lokalen Bestimmung von Strömungsgrößen oder Beschleunigungen sowie eine Strömungssensoranordnung und eine Beschleunigungssensoranordnung. Das optomechanische System umfasst eine obere und eine untere Deckschicht (210; 220), wenigstens eine zwischen den Deckschichten angeordnete, lichtleitende optische Schicht (410, 420), und wenigstens eine optomechanische Elementarzelle (400), welche ein optisches Volumen (433) sowie ein Übertragungselement (320) umfasst, das von oben mit einer Kraft beaufschlagbar ist und das auf das optische Volumen einwirken kann, wobei das optische Volumen wenigstens abschnittsweise in der optischen Schicht ausgebildet ist, um einen Quell-Lichtstrahl aus der optischen Schicht zu empfangen, so dass dieser in einen Teil des oder das gesamte optische(n) Volumen(s) eindringt, und er in Abhängigkeit von der das Übertragungselement beaufschlagenden Kraft als modifizierter Signal-Lichtstrahl aus dem optischen Volumen herausgeleitet wird.
Abstract:
The present invention relates to a method for removal of an organic amine from hydrocarbon stream containing the amine, comprising the steps of : - reacting the amine of the hydrocarbon stream containing the amine with an acid and forming an amine salt, and - extracting the amine-salt formed into an aqueous phase, wherein the hydrocarbon stream containing the amine is an outlet stream from a reactor for preparing linear alpha -olefins (LAO) by oligomerization of ethylene or a fraction of such an outlet stream, wherein the reactor contains a catalyst comprising a zirconium component and an organoaluminum component.
Abstract:
Gegenstand der Erfindung ist ein Spindelkopf für eine Universal-Fräsmaschine mit einem an einem Maschinenteil (10) verdrehbar montiertem Gehäuse (12) und einer achsparallel im Gehäuse angeordneten direktangetriebenen Arbeitsspindel (14). Gemäss der Erfindung ist an der Rückseite des Gehäuses (12) eine um zwei Achsen verstellbare zweite Spindeleinheit (15, 2) angeordnet.
Abstract:
The present invention relates to a method for the oligomerisation of ethylene, comprising the steps of: (i) oligomerising ethylene in a reactor in the presence of a solvent and a catalyst composition; (ii) discharging a catalyst composition containing outlet stream from the reactor; (iii) deactivating and extracting the catalyst composition with a polar phase, wherein the outlet stream and the polar phase are mixed in a dynamic mixing device having rotor and stator elements comprising concentric tool rings as well as to a reactor system therefore.
Abstract:
The present invention relates to a method for preparing linear alpha-olefins (LAO) by oligomerization of ethylene in the presence of solvent and homogenous catalyst, comprising the steps of: (i) feeding ethylene, solvent and catalyst into an oligomerization reactor, (ii) oligomerizing the ethylene in the reactor, (iii) removing a reactor outlet stream comprising solvent, linear alpha-olefins, ethylene, and catalyst from the reactor via a reactor outlet piping system, (iv) transferring the reactor outlet stream to a catalyst deactivation and removal step, and (v) deactivating and removing the catalyst from the reactor outlet stream, characterized in that at least one organic amine is added into the oligomerization reactor and/or into the reactor outlet piping system.
Abstract:
This invention is directed to a method of removing dimethyl ether from an olefin stream. The method includes distilling the olefin stream so that the dimethyl ether is separated out of the olefin stream with propane. The olefin stream can then be further distilled to provide a polymer grade ethylene stream and a polymer grade propylene stream, with each stream containing not greater than about 10 wppm dimethyl ether.
Abstract:
The present invention relates to a method for preparing linear alpha-olefins (LAO) by oligomerization of ethylene in the presence of a solvent and homogeneous catalyst, comprising the steps of: (i) feeding ethylene, solvent and catalyst into an oligomerization reactor, (ii) oligomerizing the ethylene in the reactor, (iii) removing a reactor outlet stream comprising solvent, linear alpha-olefins, optionally unreacted ethylene and catalyst from the reactor via a reactor outlet piping system, (iv) dosing at least one additive selected from the group consisting of alcohols, polyethylene glycols, polyethylene glycol monoethers, polyethylene glycol diethers, polyamines, amines, amino alcohols and surfactants, (v) transferring the reactor outlet stream containing the additive to a catalyst deactivation and removal section, and (vi) deactivating the catalyst with caustic and removing the deactivated catalyst from the reactor outlet stream, wherein the residence time of the additive in the reactor outlet stream prior to mixing with caustic is at least 1 second preferably at least 5 seconds, more preferably at least 10 seconds.
Abstract:
A method is described for producing olefins from methanol in a reactor, wherein liquid methanol is evaporated and introduced into the reactor as gaseous methanol for olefin synthesis, while hot olefin-containing reactor exit gas is removed from the reactor. For better utilization of heat, it is proposed to send at least a part of the liquid methanol (1) with the reactor exit gas (15) into a heat exchanger (9), where the liquid methanol (1) is evaporated and the reactor exit gas (15) is simultaneously cooled. The methanol evaporated in the way (14) can be impute to the reactor directly or after addition to another stream (3).
Abstract:
A method is described for processing an olefin-containing product stream (1) that contains, besides ethylene and propylene, longer-chain olefins and compounds of hydrocarbons with oxygen (oxygenates). Such a product stream (I) can occur in particular in olefin synthesis from methanol. The product stream is dewatered in successive process steps, optionally compressed in several steps and dried. Then it is subjected to fractionation. For removal of the undesired oxygenates it is proposed that the oxygenates be washed out of the gaseous product stream after the compression steps and before the drying step in a column (12) with methanol.
Abstract:
This invention is directed to a method of removing dimethyl ether from an olefin stream. The method includes distilling the olefin stream so that the dimethyl ether is separated out of the olefin stream with propane. The olefin stream can then be further distilled to provide a polymer grade ethylene stream and a polymer grade propylene stream, with each stream containing not greater than about 10 wppm dimethyl ether.